Method of treating titanium dioxide waste acid of sulfuric acid method using ferrous sulfate
A technology of ferrous sulfate and titanium white waste acid, which is applied in the field of titanium dioxide, can solve the problems that have not been completely solved and the blockage of graphite heaters, so as to avoid the use of boilers and evaporators, reduce pressure, and improve the working environment Effect
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Embodiment 1
[0039] 100 grams of sulfuric acid process titanium dioxide hydrolysis waste acid contains 20% sulfuric acid and 2-3% ferrous sulfate.
[0040]The first step: 100 grams of waste acid and 62 grams of ferrous sulfate monohydrate are mixed at normal temperature. After keeping for a certain period of time, the solid-liquid separation obtains 57 grams of liquid phase, and the concentration of sulfuric acid rises to 35%; obtain about 106 grams of solid phase, The solid phase is ferrous sulfate heptahydrate (FeSO 4 ·7H 2 O), after drying at 70°C to 100°C to remove 6 crystal water, return to use;
[0041] Second step: add 344 gram of ferrous sulfate anhydrous in the 57 gram liquid phases of first step gained, mix under normal temperature, after keeping certain hour, solid-liquid separation obtains 36.4 gram liquid phases, and sulfuric acid concentration is raised to 55%; Obtain about 385 grams of solid phase, the solid phase is ferrous sulfate monohydrate (FeSO 4 ·H 2 O), after dry...
Embodiment 2
[0044] Mix 100 grams of sulfuric acid titanium dioxide hydrolysis waste acid, which contains 20% sulfuric acid and 2-3% ferrous sulfate, with 510 grams of anhydrous ferrous sulfate at room temperature, keep it for a certain period of time, and separate the solid and liquid to obtain 36.4 gram liquid phase, sulfuric acid concentration is raised to 55%; Obtain about 571 gram solid phases, and this solid phase is ferrous sulfate monohydrate (FeSO 4 H2O), after drying at 300°C to 350°C to remove crystal water, return to use.
[0045] The obtained liquid phase with a mass concentration of sulfuric acid of 55% can be returned to acid hydrolysis for continuous acid hydrolysis; or be concentrated to greater than 60% with flue gas and returned for intermittent acid hydrolysis.
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